EP4508056A1 - Indole-functionalized bisphosphoramidites, methods for the preparation thereof, and rhodium-ligand complex - Google Patents
Indole-functionalized bisphosphoramidites, methods for the preparation thereof, and rhodium-ligand complexInfo
- Publication number
- EP4508056A1 EP4508056A1 EP23722180.9A EP23722180A EP4508056A1 EP 4508056 A1 EP4508056 A1 EP 4508056A1 EP 23722180 A EP23722180 A EP 23722180A EP 4508056 A1 EP4508056 A1 EP 4508056A1
- Authority
- EP
- European Patent Office
- Prior art keywords
- indole
- bis
- bisphosphoramidite
- functionalized
- formula
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
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- C07F7/00—Compounds containing elements of Groups 4 or 14 of the Periodic Table
- C07F7/02—Silicon compounds
- C07F7/08—Compounds having one or more C—Si linkages
- C07F7/0803—Compounds with Si-C or Si-Si linkages
- C07F7/0825—Preparations of compounds not comprising Si-Si or Si-cyano linkages
- C07F7/083—Syntheses without formation of a Si-C bond
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- C07F7/00—Compounds containing elements of Groups 4 or 14 of the Periodic Table
- C07F7/02—Silicon compounds
- C07F7/08—Compounds having one or more C—Si linkages
- C07F7/0834—Compounds having one or more O-Si linkage
- C07F7/0838—Compounds with one or more Si-O-Si sequences
- C07F7/087—Compounds of unknown structure containing a Si-O-Si sequence
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- C07F15/00—Compounds containing elements of Groups 8, 9, 10 or 18 of the Periodic Table
- C07F15/0006—Compounds containing elements of Groups 8, 9, 10 or 18 of the Periodic Table compounds of the platinum group
- C07F15/0073—Rhodium compounds
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- C07F7/00—Compounds containing elements of Groups 4 or 14 of the Periodic Table
- C07F7/02—Silicon compounds
- C07F7/08—Compounds having one or more C—Si linkages
- C07F7/0834—Compounds having one or more O-Si linkage
- C07F7/0838—Compounds with one or more Si-O-Si sequences
- C07F7/0872—Preparation and treatment thereof
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- C07F7/00—Compounds containing elements of Groups 4 or 14 of the Periodic Table
- C07F7/02—Silicon compounds
- C07F7/08—Compounds having one or more C—Si linkages
- C07F7/10—Compounds having one or more C—Si linkages containing nitrogen having a Si-N linkage
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- C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
- C07F9/02—Phosphorus compounds
- C07F9/547—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom
- C07F9/553—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom having one nitrogen atom as the only ring hetero atom
- C07F9/572—Five-membered rings
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- C07F9/00—Compounds containing elements of Groups 5 or 15 of the Periodic Table
- C07F9/02—Phosphorus compounds
- C07F9/547—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom
- C07F9/553—Heterocyclic compounds, e.g. containing phosphorus as a ring hetero atom having one nitrogen atom as the only ring hetero atom
- C07F9/572—Five-membered rings
- C07F9/5728—Five-membered rings condensed with carbocyclic rings or carbocyclic ring systems
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- C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
- C08G77/04—Polysiloxanes
- C08G77/14—Polysiloxanes containing silicon bound to oxygen-containing groups
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- C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
- C08G77/04—Polysiloxanes
- C08G77/20—Polysiloxanes containing silicon bound to unsaturated aliphatic groups
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- C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
- C08G77/04—Polysiloxanes
- C08G77/38—Polysiloxanes modified by chemical after-treatment
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- C08G77/00—Macromolecular compounds obtained by reactions forming a linkage containing silicon with or without sulfur, nitrogen, oxygen or carbon in the main chain of the macromolecule
- C08G77/70—Siloxanes defined by use of the MDTQ nomenclature
Definitions
- An indole-functionalized bisphosphoramidite having a certain formula is disclosed.
- the indole-functionalized bisphosphoramidite is suitable for use as a ligand, particularly for preparing a rhodium-ligand complex.
- a method of preparing a rhodium-ligand complex with the indole-functionalized bisphosphoramidite is also disclosed.
- Aldehydes are important intermediates in the synthesis of other functionalized materials like alcohols, carboxylic acids, and amines.
- the hydroformylation of olefins to prepare aldehydes is highly dependent on catalyst selection, both in terms of aldehyde selectivity (as linear aldehydes are generally preferred over branched aldehydes), production rate, and catalyst stability.
- Many conventional catalysts utilized in hydroformylation of olefins even if having desirable selectivity, have poor stability that deactivate over time, which is undesirable.
- the indole-functionalized bisphosphoramidite has a formula selected from the group consisting of C1 ), C2), or C3):
- R 1 -R 42 are each independently selected from H, a hydrocarbyl group, a heteroaryl group, a halogen atom, or a heterocarbyl group, with the proviso that at least one of R 35 -R 42 is not H.
- Each of Y 1 to Y 12 is an independently selected indole group of each of R 43 -R 47 is an independently selected atom or group selected from H, alkyl, aryl, heteroaryl, alkoxy, acyl, carboxyl, carboxylate, cyano, — SO3H, sulfonate, amino, trifluoromethyl, halogen, a group of formula (II) below, and combinations thereof.
- each of R 48 -R 52 is an independently selected atom or group selected from H, alkyl, aryl, and alkoxy; or b) two or more of R 44 -R 47 are bonded together to give one or more cyclic moieties; and ill) when the indole-functionalized bisphosphoramidite has the formula C1 ), at least one of R 44 -R 46 of at least one of Y 1 -Y 4 has formula (II).
- a method for preparing a rhodium-ligand complex comprises 1 ) combining starting materials comprising: (I) a rhodium catalyst precursor, and (II) the indole-functionalized bisphosphoramidite; and optionally (III) a solvent.
- the indole-functionalized bisphosphoramidite has a formula selected from the group consisting of C1 ), C2), or C3):
- R 1 -R 42 are each independently selected from H, a hydrocarbyl group, a heteroaryl group, a halogen atom, or a heterocarbyl group, with the proviso that at least one of R 35 -R 42 is not H. Because at least one of R 35 -R 42 is not H. at least one of R 35 -R 42 is a hydrocarbyl group, a heteroaryl group, a halogen atom, or a heterocarbyl group.
- Suitable hydrocarbyl groups for R 1 -R 42 may independently be linear, branched, cyclic, or combinations thereof. Cyclic hydrocarbyl groups encompass aryl groups as well as saturated or non-conjugated cyclic groups. Cyclic hydrocarbyl groups may be monocyclic or polycyclic. Linear and branched hydrocarbyl groups may independently be saturated or unsaturated. One example of a combination of a linear and cyclic hydrocarbyl group is an aralkyl group. By “substituted,” it is meant that one or more hydrogen atoms may be replaced with atoms other than hydrogen (e.g. a halogen atom, such as chlorine, fluorine, bromine, etc.).
- Suitable alkyl groups are exemplified by, but not limited to, methyl, ethyl, propyl (e.g., iso-propyl and/or n-propyl), butyl (e.g., isobutyl, n-butyl, tert-butyl, and/or sec-butyl), pentyl (e.g., isopentyl, neopentyl, and/or tert-pentyl), hexyl, as well as branched saturated hydrocarbon groups of 6 carbon atoms.
- propyl e.g., iso-propyl and/or n-propyl
- butyl e.g., isobutyl, n-butyl, tert-butyl, and/or sec-butyl
- pentyl e.g., isopentyl, neopentyl, and/or tert-pentyl
- Suitable aryl groups are exemplified by, but not limited to, phenyl, tolyl, xylyl, naphthyl, benzyl, and dimethyl phenyl.
- Suitable alkenyl groups include vinyl, allyl, propenyl, isopropenyl, butenyl, isobutenyl, pentenyl, heptenyl, hexenyl, and cyclohexenyl groups.
- Suitable monovalent halogenated hydrocarbon groups include, but are not limited to, a halogenated alkyl group of 1 to 6 carbon atoms, or a halogenated aryl group of 6 to 10 carbon atoms.
- Suitable halogenated alkyl groups are exemplified by, but not limited to, the alkyl groups described above where one or more hydrogen atoms is replaced with a halogen atom, such as F or Cl.
- a halogen atom such as F or Cl.
- Suitable halogenated aryl groups are exemplified by, but not limited to, the aryl groups described above where one or more hydrogen atoms is replaced with a halogen atom, such as F or Cl.
- a halogen atom such as F or Cl.
- chlorobenzyl and fluorobenzyl are suitable halogenated aryl groups.
- Suitable heterocarbyl groups include any of the hydrocarbyl groups described above, but including one or more heteroatoms, such as oxygen, sulfur, nitrogen, etc.
- Suitable halogen atoms include F, Cl, Br, I, At, and Ts, alternatively F, Cl, and Br, alternatively Cl.
- Each of Y 1 to Y 12 is an independently selected indole group of formula (I): where each of R 43 -R 47 is an independently selected atom or group selected from H, alkyl, aryl, heteroaryl, alkoxy, acyl, carboxyl, carboxylate, cyano, — SO3H, sulfonate, amino, trifluoromethyl, halogen, a group of formula (II) below, and combinations thereof. Examples of alkyl, aryl, and heteroaryl are described above. In the formula above, the single line attached to N represents a bond, as the formula above is monovalent.
- R 43 -R 47 has formula each of R 48 -R 52 is an independently selected atom or group selected from H, alkyl, aryl, and alkoxy; or b) two or more of R 44 -R 47 are bonded together to give one or more cyclic moieties; and ill) when the indole-functionalized bisphosphoramidite has the formula C1 ), at least one of R 44 -R 46 of at least one of Y 1 -Y 4 has formula (II).
- provisos (i) to (iii) apply to the indole-functionalized bisphosphoramidite.
- provisos (ii)(a) and (ii)(b) need apply, i.e., both of (ii)(a) and (ii)(b) are not required, as these are alternative requirements, and thus only one of (ii)(a) or (ii)(b) is required.
- provisos (i) to (iii) apply to the indole-functionalized bisphosphoramidite, proviso (iii) is only invoked if the indole-functionalized bisphosphoramidite is of formula C1). Provisos (ii)(a) and (iii) are relevant to one another but apply to different embodiments of the indole-functionalized bisphosphoramidite.
- R 43 -R 47 has formula (II) (i.e., proviso (ii)(a)), or two or more of R 44 -R 47 are bonded together to give one or more cyclic moieties (i.e., proviso (ii)(b)).
- R 43 of at least one of Y 1 -Y 4 can still be of formula (II), so long as at least one of R 44 -R 46 of at least one of Y 1 -Y 4 also has formula (II).
- formula (II) is independently selected from one of the following formulas:
- the single line attached to each aryl moiety represents a bond in the indole group of formula (I), rather than a methyl group, as the formulas above are monovalent.
- Methyl groups are expressly labeled as such.
- each of Y 1 to Y 12 can independently be selected from the group consisting of (subject to the provisos, and where Me means methyl, OMe means methoxy, Ph means phenyl, and tBu means t-butyl):
- one example of Y 1 to Y 12 is: [0018]
- at least one of R 44 -R 46 has formula (II).
- R 44 has formula (II).
- R 45 has formula (II).
- proviso (ii)(a) is true
- R 46 has formula (II).
- the indole-functionalized bisphosphoramidite has formula C1), and each of R 1 -R 20 is H. In other embodiments, the indole-functionalized bisphosphoramidite has formula C2), and each of R 21 -R 34 is H. In yet other embodiments, the indole-functionalized bisphosphoramidite has formula C3), and each of R 35 and R 42 is H, and each of R 36 -R 41 is methyl.
- the indole-functionalized bisphosphoramidite has formula C1). In another embodiment, the indole-functionalized bisphosphoramidite has formula C2). In yet another embodiment, the indole-functionalized bisphosphoramidite has formula C3).
- indole-functionalized bisphosphoramidite has formula C1)
- R 1 - R 20 are each H
- the indole-functionalized bisphosphoramidite of formula C1 becomes the following: where Y 1 -Y 4 are independently selected and defined above.
- indole-functionalized bisphosphoramidite has formula C2)
- R 21 -R 34 are each H
- the indole-functionalized bisphosphoramidite of formula C2) becomes the following: where Y 5 -Y 8 are independently selected and defined above.
- R 35 and R 42 are H, and each of R 36 -R 41 is methyl, the indole-functionalized bisphosphoramidite of formula C3) becomes the following: where Y 9 -Y 12 are independently selected and defined above.
- the indole-functionalized bisphosphoramidite has formula C1 ), provisos (i), (ii)(a), and (iii) apply, and R 1 -R 20 and Y 1 -Y 4 are selected such that the indole-functionalized bisphosphoramidite is selected from the group consisting of those below in Table 1 (L1 -L9 or L13).
- the indole-functionalized bisphosphoramidite has formula C1), provisos (i), (ii)(b), and (iii) apply, and R 1 -R 20 and Y 1 -Y 4 are selected such that the indole- functionalized bisphosphoramidite has the following formula below in Table 2 (L12).
- the indole-functionalized bisphosphoramidite has formula C2), and R 21 -R 34 , and Y 5 -Y 8 are selected such that the indole-functionalized bisphosphoramidite has the following formula below in Table 3 (L11 ).
- the indole-functionalized bisphosphoramidite has formula C3), and R 35 -R 42 , and Y 9 -Y 12 are selected such that the indole-functionalized bisphosphoramidite has the following formula below in Table 4 (L10).
- a method for preparing a rhodium-ligand complex comprises combining starting materials comprising: (I) a rhodium catalyst precursor, and (II) the indole-functionalized bisphosphoramidite; and optionally (III) a solvent.
- the rhodium- ligand complex forms from starting materials (I) and (II), optionally in starting material (III).
- the rhodium-ligand complex may be prepared by a process comprising combining a rhodium catalyst precursor and the indole-functionalized bisphosphoramidite described above under conditions to form the complex.
- the rhodium-ligand complex may be formed in situ by introducing the rhodium catalyst precursor into a reaction medium, and the indole-functionalized bisphosphoramidite into the reaction medium (e.g., before, during, and/or after introduction of the rhodium catalyst precursor), for the in situ formation of the rhodium-ligand complex, e.g. during a hydroformylation reaction, as described below.
- Rhodium catalyst precursors are exemplified by rhodium dicarbonyl acetylacetonate, Rh 2 O 3 , Rh 4 (CO)i2, Rh s (CO) 16, and Rh(NO 3 ) 3 . Additional methods to prepare certain indole- functionalized bisphosphoramidites are described herein in the appended Examples.
- a rhodium catalyst precursor such as rhodium dicarbonyl acetylacetonate, optionally starting material (D), a solvent, and the indole-functionalized bisphosphoramidite may be combined, e.g., by any convenient means such as mixing.
- the rhodium-ligand complex is particularly suited for a hydroformylation process involving an olefin.
- the hydroformylation process described herein employs starting materials comprising: (A) a gas comprising hydrogen and carbon monoxide, (B) an olefin, and (C) the rhodium-ligand complex catalyst.
- the starting materials may optionally further comprise (D) a solvent.
- Starting material (A), the gas used in the hydroformylation process, comprises carbon monoxide (CO) and hydrogen gas (H 2 ).
- the gas may be syngas.
- syngas (from synthesis gas) refers to a gas mixture that contains varying amounts of CO and H 2 . Production methods are well known and include, for example: (1 ) steam reforming and partial oxidation of natural gas or liquid hydrocarbons, and (2) the gasification of coal and/or biomass.
- CO and H 2 typically are the main components of syngas, but syngas may contain carbon dioxide and inert gases such as CH 4 , N 2 and Ar.
- the molar ratio of H 2 to CO (H 2 :CO molar ratio) varies greatly but may range from 1 :100 to 100:1 , alternatively 1 :10 and 10:1 .
- Syngas is commercially available and is often used as a fuel source or as an intermediate for the production of other chemicals.
- CO and H 2 from other sources i.e., other than syngas
- the H 2 :CO molar ratio in starting material (A) for use herein may be 3:1 to 1 :3, alternatively 2:1 to 1 :2, and alternatively 1 :1 .
- Starting material (B), the olefin, is not limited.
- Starting material (B) can be terminally or internally unsaturated and be of straightchain, branched chain, or cyclic structures.
- Olefin mixtures such as obtained from the oligomerization of propene, butene, and isobutene, (such as, so called dimeric, trimeric or tetrameric propylene) may also be employed, as well as mixed butenes, for example, raffinate I and raffinate II known to one of skill in the art.
- alpha and internal olefins suitable for starting material (B) include ethylene, propylene, 1 -butene, 1 -pentene, 1 -hexene, 1 -heptene, 1 -octene, 1 -nonene, 1 -decene, 1 -undecene, 1 -dodecene, 1 -tridecene, 1 -tetradecene, 1 -pentadecene, 1 - hexadecene, 1 -heptadecene, 1 -octadecene, 1 -nonadecene, 1 -eicosene, 2-butene, 2-methyl propene (isobutylene), 2-methylbutene, 2-pentene, 2-hexene, 3-hexane, 2-heptene, 2-octene, cyclohexene, propylene dim
- the (C) rhodium-ligand complex is described above and may be introduced into the reactor, optionally with excess indole-functionalized bisphosphoramidite.
- the rhodium catalyst precursor, (D) the solvent, and the ligand may be combined in the reactor with starting material (A) and/or (B), the olefin; and the rhodium-ligand complex may form in situ.
- the relative amounts of ligand and rhodium catalyst precursor are sufficient to provide a molar ratio of indole-functionalized bisphosphoramidite/Rh of 10/1 to 1/1 , alternatively 5/1 to 1/1 , alternatively 3/1 to 1/1 , alternatively 2.5/1 to 1.5/1.
- excess e.g., not complexed indole-functionalized bisphosphoramidite may be present in the reaction mixture.
- the excess indole-functionalized bisphosphoramidite may be the same as, or different from, the indole-functionalized bisphosphoramidite in the rhodium- ligand complex.
- the amount of (C) the rhodium-ligand complex catalyst is sufficient to catalyze hydroformylation of (B) the olefin.
- the exact amount of catalyst will depend on various factors including the type of olefin selected for starting material (B), its exact vinyl content, and the reaction conditions such as temperature and pressure of starting material (A).
- the amount of (C) the catalyst may be sufficient to provide a rhodium metal concentration of at least 0.1 ppm, alternatively 0.15 ppm, alternatively 0.2 ppm, alternatively 0.25 ppm, and alternatively 0.5 ppm, based on the weight of (B) the olefin.
- the amount of (C) the catalyst may be sufficient to provide a rhodium metal concentration of up to 300 ppm, alternatively up to 100 ppm, alternatively up to 20 ppm, and alternatively up to 5 ppm, on the same basis.
- the amount of (C) the catalyst may be sufficient to provide 0.1 ppm to 300 ppm, alternatively 0.2 ppm to 100 ppm, alternatively, 0.25 ppm to 20 ppm, and alternatively 0.5 ppm to 5 ppm, based on the weight of (B) the olefin.
- the hydroformylation process reaction may run without additional solvents.
- the hydroformylation process reaction may be carried out with a solvent, for example to facilitate mixing and/or delivery of one or more of the starting materials described above, such as (C) the catalyst and/or starting material (B).
- the solvent is exemplified by aliphatic or aromatic hydrocarbons, which can dissolve the starting materials, e.g., toluene, xylene, benzene, hexane, heptane, decane, cyclohexane, or a combination of two or more thereof.
- Additional solvents include THF, dibutyl ether, diglyme, and Texanol.
- solvent may be used to reduce the viscosity of the starting materials.
- the amount of solvent is not critical, however, when present, the amount of solvent may be 5% to 70% based on weight of starting material (B) the olefin.
- step 1 is performed at relatively low temperature.
- step 1 ) may be performed at a temperature of at least 30 °C, alternatively at least 50 °C, and alternatively at least 70 °C.
- the temperature in step 1) may be up to 150 °C; alternatively up to 100 °C; alternatively up to 90 °C, and alternatively up to 80 °C.
- lower temperatures e.g., 30 °C to 90 °C, alternatively 40 °C to 90 °C, alternatively 50 °C to 90 °C, alternatively 60 °C to 90 °C, alternatively 70 °C to 90 °C, alternatively 80 °C to 90 °C, alternatively 30 °C to 60 °C, alternatively 50 °C to 60 °C may be desired for achieving high selectivity and ligand stability.
- step 1 may be performed at a pressure of at least 101 kPa (ambient), alternatively at least 206 kPa (30 psi), and alternatively at least 344 kPa (50 psi).
- pressure in step 1) may be up to 6,895 kPa (1 ,000 psi), alternatively up to 1 ,379 kPa (200 psi), alternatively up to 1000 kPa (145 psi), and alternatively up to 689 kPa (100 psi).
- step 1 may be performed at 101 kPa to 6,895 kPa; alternatively 344 kPa to 1 ,379 kPa; alternatively 101 kPa to 1 ,000 kPa; and alternatively 344 kPa to 689 kPa.
- relatively low pressures e.g., ⁇ to 6,895 kPa in the process herein may be beneficial; the ligands described herein allow for low pressure hydroformylation processes, which have the benefits of lower cost and better safety than high pressure hydroformylation processes.
- the hydroformylation process may be carried out in a batch, semi-batch, or continuous mode, using one or more suitable reactors, such as a fixed bed reactor, a fluid bed reactor, a continuous stirred tank reactor (CSTR), or a slurry reactor.
- suitable reactors such as a fixed bed reactor, a fluid bed reactor, a continuous stirred tank reactor (CSTR), or a slurry reactor.
- the selection of (B) the olefin, and (C) the catalyst, and whether (D) the solvent, is used may impact the size and type of reactor used.
- One reactor, or two or more different reactors, may be used.
- the hydroformylation process may be conducted in one or more steps, which may be affected by balancing capital costs and achieving high catalyst selectivity, activity, lifetime, and ease of operability, as well as the reactivity of the particular starting materials and reaction conditions selected, and the desired product.
- the hydroformylation process may be performed in a continuous manner.
- the process used may be as described in U.S. Patent 10,023,516 except that the catalyst described therein is replaced with (C) the rhodium-ligand complex described herein.
- Step 1 ) of the hydroformylation process forms a reaction fluid comprising an aldehyde- functional compound.
- the reaction fluid may further comprise additional materials, such as those which have either been deliberately employed, or formed in situ, during step 1 ) of the process.
- additional materials such as those which have either been deliberately employed, or formed in situ, during step 1 ) of the process.
- materials that can also be present include unreacted (B) olefin, unreacted (A) carbon monoxide and hydrogen gases, and/or in situ formed side products, such as indole-functionalized bisphosphoramidite degradation products and adducts thereof, and high boiling liquid aldehyde condensation byproducts, as well as (D) a solvent, if employed.
- indole-functionalized bisphosphoramidite degradation product includes but is not limited to any and all compounds resulting from one or more chemical transformations of at least one of the ligand molecules used in the process.
- the hydroformylation process may further comprise one or more additional steps such as: 2) recovering (C) the rhodium-ligand complex from the reaction fluid comprising the aldehyde-functional compound.
- Recovering (C) the rhodium-ligand complex may be performed by methods known in the art, including but not limited to adsorption and/or membrane separation (e.g., nanofiltration). Suitable recovery methods are as described, for example, in U.S. Patents 5,681 ,473 to Miller, et al.; 8,748,643 to Priske, et al.; and 10,155,200 to Geilen, et al.
- the hydroformylation process may further comprise 3) purification of the reaction product.
- the aldehyde-functional compound may be isolated from the additional materials, described above, by any convenient means such as stripping and/or distillation, optionally with reduced pressure.
- LC- MS analyses were performed using a Waters e2695 Separations Module coupled with a Waters 2424 ELS detector, a Waters 2998 PDA detector, and a Waters 3100 ESI mass detector.
- LC-MS separations were performed on an XBridge C18 3.5 m 2.1 x50 mm column using a 5:95 to 100:0 acetonitrile to water gradient with 0.1 % formic acid as the ionizing agent.
- HRMS analyses were performed using an Agilent 1290 Infinity LC with a Zorbax Eclipse Plus C18 1 .8pm 2.1x50 mm column, coupled with an Agilent 6230 TOF Mass Spectrometer with electrospray ionization.
- Chemical shifts for 1 H NMR data are reported in ppm in the deuterated solvent as references.
- 1 3 C NMR data were determined with 1 H decoupling, and the chemical shifts are reported in ppm relative to tetramethylsilane (TMS, 5 scale) using residual carbons in the deuterated solvent as references.
- Chemical shifts for 31 p NMR data chemical shifts are reported in ppm (referenced with respect to H3PO4).
- phosphorus trichloride (0.36 g, 2.65 mmol) and triethylamine (1.08 g, 10.62 mmol) were added to 75 mL of toluene in a 1 10 ml_ glass jar.
- the solution was placed in the glove box freezer (-35 °C) for 1 hour to chill.
- the indole 3a (1.25 g, 5.31 mmol) was weighed into a 20 mL vial and dissolved in 10 mL of toluene.
- the indole solution was also chilled in the glove box freezer for 1 hour.
- Triethylamine (0.2 g) was added drop wise with stirring to the solution, resulting in immediate formation of a white precipitate.
- the reaction mixture was allowed to stir at room temperature and slowly warmed up to 50 °C overnight. The next morning, an aliquot of the reaction mixture was removed, filtered, and analyzed by 31 P NMR spectroscopy. 3 ⁇ P NMR shows full conversion to the desired bisphosphoramidite product with some cyclic phosphoramidite and triphosphoramidite products.
- the solid was purified by neutral alumina chromatography to yield 200 mg (30% yield) of the product (Ligand L1 ).
- phosphorus trichloride (0.34 ml_, 3.9 mmol) and triethylamine (2.5 ml_, 18 mmol) were added to 70 mL of toluene in a 1 10-mL glass jar.
- the solution was placed in the glove box freezer (-35 °C) for 1 hour to chill.
- 6-(3,5-Dimethylphenyl)-1 /-/-indole 3b (1 .75 g) was weighed into a 20 mL vial and dissolved in 15 mL of toluene.
- the indole solution was also chilled in the glove box freezer for 1 hour.
- reaction mixture was allowed to stir at room temperature overnight. The next morning, an aliquot of the reaction mixture was removed, filtered, and analyzed by 31 p NMR spectroscopy. The spectrum showed conversion to the desired product (L2, 105 ppm) in approximately 60% purity.
- the reaction mixture was filtered through Celite to remove triethylammonium chloride and the yellow filtrate was pumped down to dryness.
- the material was loaded on a 24 g Gold silica column and eluted with pure hexanes for 10 column volumes. Chloroform was then introduced to the eluent, gradually increasing to 20% chloroform (80% hexanes) over five column volumes. This solvent mixture (20/80) was used for another 10 column volumes.
- a 3-neck 2-L round bottom flask was charged with 25 g (155.3 mmol) of 1 H-indole-6-boronic acid (1a), 2.7 g (3.1 mmol) of Precatalyst, and 500 mL of THF. The mixture was stirred at room temperature. After 5 minutes, 41 .2 g (170.8 mmol) of 1 -bromo-3,5-di-tert-butylbenzene (2c) was added to the solution, followed by approximately 600 mL of an aqueous solution of potassium phosphate tribasic (99 g, 466 mmol in 600 mL of H 2 O). The reaction mixture was then stirred at room temperature overnight.
- Trituration Procedure Hexane (300 mL, ⁇ 10 ml/g crude material) was added to the crude material. The mixture was heated in a water bath (55 °C) for 15 mins to dissolve the non-polar impurities and the mixture was quickly filtered with a frit filter to collect the pure product. Following the first trituration, 23.0 g of pure product 3c was isolated as white powder. The filtrate from the first trituration was concentrated on a rotary evaporator to leave a solid residue which was purified by silica gel column chromatography using hexane:ethyl acetate as eluent to yield a second batch of the product (3c, 7.5 g) as a white solid.
- Triethylamine (34 mL, 245.5 mmol) in toluene (50 mL) was charged to a 1 10-mL glass jar and chilled inside the glove box refrigerator.
- PCI3 (3.6 mL, 41 .1 mmol) charged to a 1 -L roundbottom flask along with 50 mL of toluene was placed in the glove box refrigerator at the same time. After an hour, both the solutions were taken out of the refrigerator and the triethylamine solution was slowly added to the PCI3 solution. An additional 175 mL chilled toluene was added to the flask to keep the concentration at around 0.2 M (with respect to the PCI3).
- the 6-(3,5-di-tert-butyl)-1 H-indole (3c, 25.0 g, 81.8 mmol) was weighed into a 1 10 mL glass jar and slowly added portion-wise to the cold PCIs/NEts solution with vigorous stirring over a period of 0.5-1 h. A white precipitate started forming during the addition.
- the reaction mixture was allowed to warm to room temperature and was stirred for another 12 h. The reaction progress was monitored by 3 ⁇ P NMR. The next day, an aliquot of the reaction mixture was removed, filtered and analyzed by 3 ⁇ P NMR spectroscopy.
- the NMR shows formation of the desired mono-chlorophosphoramidite (4c, 5 108.17 ppm) as the major product along with a minor amount of tri(indolyl)phosphine (8 70.95 ppm).
- the crude reaction mixture was passed through a CeliteTM pad. The filtrate was transferred to a 1 L flask and concentrated down to a 200 mL volume using the glove box vacuum pump (vacuum trap cooled with liquid nitrogen). The crude reaction mixture was sampled for 31 p NMR and then used directly in the next step.
- reaction mixture was taken out from the glovebox and passed through a CeliteTM pad to remove all the inorganic salts; the filtrate volatiles were removed on a rotary evaporator to leave an orange foamy solid.
- This crude material was divided into two batches (each batch approximately ⁇ 10-12 g crude material) for silica gel chromatography.
- the PCl3/NEt3 solution was removed from the freezer and the indole solution was added drop wise (by an additional funnel) with stirring to the cold PCIg/NEtg solution. A copious amount of white precipitate formed during the addition.
- the reaction mixture was allowed to warm to room temperature and stirred overnight. The next day, an aliquot of the reaction mixture was removed, filtered and analyzed by 31 p NMR spectroscopy. The NMR spectrum showed formation of the desired mono-chlorophosphoramidite (5 105.61 ppm) as the major product, along with the bis-chloro compound as the minor product (0 145.42 ppm).
- Triethylamine (3.4 mL, 24.5 mmol) was added dropwise with stirring to the solution, resulting in immediate formation of a white precipitate.
- the reaction mixture was allowed to stir at room temperature and slowly warmed up to 50 °C overnight. The next morning, an aliquot of the reaction mixture was removed, filtered, and analyzed by 31 p NMR spectroscopy; full conversion to products (5 111.01 ppm) with some cyclic phosphoramidite product (5 128.22 ppm) was indicated. Two step purification was required to remove all the attendant by-products.
- a 330 g gold silica gel column (5-30 % dichloromethane in hexane) was utilized to purify the bis-product with the rest of the side products.
- a 160 g neutral alumina column was utilized to further purify the bisphosphoramidite product from the indole side product (5-20 % dichloromethane in hexane). After column purification, 1 .9 g of pure bisphosphoramidite product (Ligand L4) was obtained with 24 % yield.
- a 3-neck 2-L round bottom flask was charged with 2 g (12.4 mmol) of 1 H-indole-6-boronic acid (1a), 0.2 g (0.25 mmol) of Precatalyst, and 80 mL of THF. The mixture was stirred at room temperature. After 5 minutes, 3.0 g (13.7 mmol) of 1 -bromo-3,5-di-methoxy-benzene (2e) was added to the solution, followed by approximately 50 mL of an aqueous solution of potassium phosphate tribasic (7.9 g, 38 mmol in 25 mL of H2O). The reaction mixture was then stirred at room temperature overnight.
- phosphorus trichloride 0.3 ml_, 3.2 mmol
- triethylamine 2.7 ml_
- the solution was placed in the glove box freezer (-35 °C) for 1 hour to chill.
- the 6-(3,5-di-methoxy-phenyl)-1 H-indole (3e, 1 .65 g, 6.5 mmol) was weighed into a 50-mL glass jar and dissolved in 10 mL of toluene.
- the PCIg/NEtg solution was removed from the freezer and the indole solution was added drop wise (by an additional funnel) with stirring to the cold PCIg/NEtg solution. A copious amount of white precipitate formed during the addition.
- the reaction mixture was allowed to warm to room temperature and stirred overnight. The next day, an aliquot of the reaction mixture was removed, filtered and analyzed by 31 p NMR spectroscopy. The NMR spectrum showed formation of the desired mono-chlorophosphoramidite (d 102.64 ppm) as the major product.
- the crude mixture was filtered through a plug of Celite to remove the inorganic salts and the filtrate was further evaporated using glove box vacuum pump (keeping liquid nitrogen in the trap) to obtain the desired mono-chlorophosphoramidite as a yellowish powder (>90% yield).
- the compound was directly used on next step without further purification.
- reaction mixture was allowed to stir at room temperature and slowly warmed up to rt overnight. The next morning, an aliquot of the reaction mixture was removed, filtered, and analyzed by 31 p NMR spectroscopy; full conversion to the product, bisphosphoramidite (5 109.00 ppm) with some cyclic phosphoramidite (5 129.16 ppm) was indicated.
- the reaction mixture was passed over Celite pad, washed with toluene and the filtrate was concentrated down to reddish oil.
- Silica gel purification was required to remove all of the attendant by-products. A 330 g gold silica gel column (50-100% dichloromethane in hexane) was utilized to purify the desired product with the rest of the side products, After column purification, 0. 5 g of pure bisphosphoramidite product (Ligand L5) was obtained with 25 % yield.
- phosphorus trichloride 0.52 ml_, 5.9 mmol
- triethylamine 4.9 ml_
- the solution was placed in the glove box freezer (-35 °C) for 1 hour to chill.
- the 6-(4-tert-butyl-phenyl)-1 H-indole (3f, 4.1 g, 11.87 mmol) was weighed into a 50 mL glass jar and dissolved in 10 mL of toluene.
- the PCl3/NEt3 solution was removed from the freezer and the indole solution was added drop wise (by an additional funnel) with stirring to the cold PCIs/NEts solution. A copious amount of white precipitate formed during the addition.
- the reaction mixture was allowed to warm to room temperature and stirred overnight. The next day, an aliquot of the reaction mixture was removed, filtered and analyzed by 31 p NMR spectroscopy. The NMR spectrum showed formation of the desired mono-chlorophosphoramidite (5 100.99 ppm) as the major product.
- the crude mixture was filtered through a plug of Celite to remove the inorganic salts and the filtrate was further evaporated using glove box vacuum pump (keeping liquid nitrogen in the trap) to obtain the desired mono-chlorophosphoramidite as a brownish powder.
- the compound was directly used on next step without further purification.
- Triethylamine (1 .4 ml_) was added drop wise with stirring to the solution, resulting in immediate formation of a white precipitate.
- the reaction mixture was allowed to stir at room temperature and slowly warmed up to 50 °C overnight. The next morning, an aliquot of the reaction mixture was removed, filtered, and analyzed by 31 P NMR spectroscopy. 31 p NMR shows full conversion to the desired bisphosphoramidite product with some cyclic phosphoramidite and triphosphoramidite products.
- the solid was purified by silica gel chromatography to yield 240 mg (11% yield) of the product (Ligand L6).
- Preparation Example 7 Ligand 7 A 3-neck 250 mL round bottom flask was charged with 2 g (12.4 mmol) of 1 /-/-indole-6-boronic acid (1a), 0.2 g (0.25 mmol) of Precatalyst, and 80 mL of THF. The mixture was stirred for 5 minutes at room temperature. After 5 minutes, 2.5 g (13.7 mmol) of 4-bromoanisole (2g) was added to the solution, followed by approximately 50 mL of an aqueous solution of potassium phosphate tribasic (7.9 g, 38mmol) in 25 mL of H2O). The reaction mixture was then stirred at room temperature overnight.
- phosphorus trichloride 0.3 mL, 3.2 mmol
- triethylamine 2.7 mL
- the solution was placed in the glove box freezer (-35 °C) for 1 hour to chill.
- the 6-(4-methoxyphenyl)-1 H-indole (3g, 1 .45 g, 6.5 mmol) was weighed into a 50 mL glass jar and dissolved in 10 mL of toluene.
- the PCIg/NEtg solution was removed from the freezer and the indole solution was added drop wise (by an additional funnel) with stirring to the cold PCIg/NEtg solution. A copious amount of white precipitate formed during the addition.
- the reaction mixture was allowed to warm to room temperature and stirred overnight. The next day, an aliquot of the reaction mixture was removed, filtered and analyzed by 31 p NMR spectroscopy. The NMR spectrum showed formation of the desired mono-chlorophosphoramidite (d 103.29 ppm) as the major product.
- the crude mixture was filtered through a plug of Celite to remove the inorganic salts and the filtrate was further evaporated using glove box vacuum pump (keeping liquid nitrogen in the trap) leaving 3.1 g of the desired mono-chlorophosphoramidite as a yellowish powder (>90% yield).
- the compound was directly used on next step without further purification.
- Triethylamine (1.2 mL) was added dropwise with stirring to the solution, resulting in immediate formation of a white precipitate.
- the reaction mixture was allowed to stir at room temperature and slowly warmed up to 50 °C overnight. The next morning, an aliquot of the reaction mixture was removed, filtered, and analyzed by 31 p NMR spectroscopy; full conversion to bisphosphoramidite product (5 104.37 ppm).
- Two step purification was required to remove all of the attendant by-products. In a first step, a 330 g gold silica gel column (5 - 20 % dichloromethane in hexane) was utilized to purify the bis product with the rest of the side products.
- a 160 g neutral alumina column was utilized to further purify the bisphosphoramidite product from the indole side product (5 - 20 % dichloromethane in hexane). After column purification, 0.6 g of pure bisphosphoramidite product (Ligand L7) was obtained with 35 % yield.
- the substituted indole 3h (2 equivalents) was weighed into a 110 mL glass jar, dissolved in a minimum amount of toluene and slowly added to the cold PCl3/NEt3 solution with vigorous stirring over a period of 15-30 min. A white precipitate started forming during the addition.
- the reaction mixture was allowed to warm to room temperature and was stirred for another 12 h. The reaction progress was monitored by 31 p NMR. The next day, an aliquot of the reaction mixture was removed, filtered and analyzed by 31 p NMR to confirm formation of the desired bis(indolyl)chlorophosphine 4h as the major product.
- the crude reaction mixture was passed through a CeliteTM pad to remove the inorganic salts, and the filtrate was transferred to a 220 mL glass jar and concentrated to approximately 1 /4th of its original volume using the glove box vacuum pump (vacuum trap cooled with liquid nitrogen).
- the crude reaction mixture was sampled for 31 p NMR and used directly in the next step.
- the substituted indole 3i (2 equivalents) was weighed into a 110 mL glass jar, dissolved in a minimum amount of toluene and slowly added to the cold PC ⁇ /NEts solution with vigorous stirring over a period of 15-30 min. A white precipitate started forming during the addition.
- the reaction mixture was allowed to warm to room temperature and was stirred for another 12 h. The reaction progress was monitored by 31 p NMR. The next day, an aliquot of the reaction mixture was removed, filtered and analyzed by 31 p NMR to confirm formation of the desired bis(indolyl)chlorophosphine 4h as the major product.
- the crude reaction mixture was passed through a CeliteTM pad to remove the inorganic salts, and the filtrate was transferred to a 220 mL glass jar and concentrated to approximately 1 /4th of its original volume using the glove box vacuum pump (vacuum trap cooled with liquid nitrogen).
- the crude reaction mixture was sampled for 31 p NMR and used directly in the next step.
- Triethylamine (1 .6 mL, 11.1 mmol) was added dropwise with stirring to the solution, resulting in immediate formation of a white precipitate.
- the reaction mixture was allowed to stir at room temperature and slowly warmed up to 50 °C overnight. The next morning, an aliquot of the reaction mixture was removed, filtered, and analyzed by 31 p NMR. Two step purification was required to remove all of the attendant by-products. In a first step, a 330 g gold silica gel column (5 - 20 % dichloromethane in hexane) was utilized to purify the bis product with the rest of the side products.
- a 160 g neutral alumina column was utilized to further purify the bisphosphoramidite product (5 - 20 % dichloromethane in hexane). After column purification, 1.2 g of pure bisphosphoramidite ligand L10 was obtained with 28 % yield.
- reaction mixture was allowed to stir at room temperature and slowly warmed up to rt overnight. The next morning, an aliquot of the reaction mixture was removed, filtered, and analyzed by 31 p NMR spectroscopy; the reaction was very clean and only one major peak (5 6 105.28 ppm) with some minor products were observed.
- the glass jar was taken out from the glove-box and the reaction mixture was passed over a celite pad. The filtrate was concentrated down and loaded directly over to 330g silica column using liquid injection. Silica gel column was required to remove all of the attendant byproducts.
- phosphorus trichloride (0.6 mL, 7.0 mmol) and triethylamine (3.0 mL) were added to 20 mL of toluene in a 110 mL glass jar.
- the solution was placed in the glove box freezer (-35 °C) for 1 hour to chill.
- the 6,7-fused-1 H-indole (3I, 1 .1 g, 7.0 mmol) was weighed into a 50 mL glass jar and dissolved in 15 mL of toluene.
- the PCIg/NEtg solution was removed from the freezer and the indole solution was added drop wise with stirring to the cold PCIg/NEtg solution.
- the reaction mixture was allowed to warm to room temperature and stirred for another 3 h. After 3 h, an aliquot of the reaction mixture was removed, filtered and analyzed by 31 p NMR spectroscopy. The NMR spectrum showed formation of the desired di- chloroindolylphosphine 4I’ (5 147.30 ppm) as the major product.
- the crude NMR was clean enough to move forward for the next step.
- the crude mixture was filtered through a plug of Celite to remove the inorganic salts and the filtrate was further concentrated using glove box vacuum pump (keeping liquid nitrogen in the trap) to 10 mL solution.
- the di-chloroindolylphosphine solution (41’) was kept in the in the glove box freezer (-35 °C) for 1 hour to chill.
- the 1 /-/-indole (0.82 g, 7.0 mmol) was weighed into a 50 mL glass jar and dissolved in 15 mL of toluene.
- the di-chloroindolylphosphine solution was removed from the freezer and 3.0 mL triethylamine was added to the solution.
- indole solution was added drop wise with stirring to the reaction solution.
- the reaction mixture was allowed to warm to room temperature and stirred for another 3 h.
- the two solutions were removed from the freezer and the cold indole solution was added drop wise (by an additional funnel) with stirring to the cold PCl3/NEt3 solution. A copious amount of white precipitate formed during the addition.
- the reaction mixture was allowed to warm to room temperature and stir overnight at 60 °C. The next day, an aliquot of the reaction mixture was removed, filtered and analyzed by 31 p NMR spectroscopy. The NMR shows formation of the desired mono-chlorophosphoramidite (5 102.43 ppm) as the major product, however it also showed the bis-chloro product as the minor product (0 143.52 ppm).
- reaction was further analyzed by 31 p NMR spectroscopy.
- the reaction showed complete conversion to the desired mono- chlorophosphoramidite (5 102.43 ppm) as the major product with ⁇ 4-5% bis-chloro product as the minor product (5 143.52 ppm).
- the crude mixture was filtered through a plug of Celite to remove the inorganic salts and the filtrate was further evaporated using glove box vacuum pump (keeping liquid nitrogen trap) and 4.4 g of the desired mono-chlorophosphoramidite (4m) was isolated as a yellowish powder (>90% yield).
- Triethylamine (2.0 mL) was added drop wise with stirring to the solution, resulting in immediate formation of a white precipitate.
- the reaction mixture was allowed to stir at room temperature and slowly warmed up to 50 °C overnight. The next morning, an aliquot of the reaction mixture was removed, filtered, and analyzed by 31 P NMR spectroscopy.
- 31 P NMR shows full conversion to product (5 107.89 ppm) with some mono-alcohol and cyclic phosphoramidite products.
- Two step purification was used to remove all the indole side products. In particular, a 1 st column purified the bis product with the rest of the side products (silica gel column), and a 2nd column purified the bis product from the indole side product (alumina column).
- the reaction mixture was then allowed to stirred overnight at room temperature. The next day an aliquot was removed, worked up with diethyl ether and checked by mass spectroscopy. The reaction was complete, stopped and removed from the glovebox. Diethyl ether (50 mL) was added to the reaction mixture and then transferred a separatory funnel. The aqueous layer was then washed with equal parts of diethyl ether (2X). The organic layers were then combined, dried over MgSC j. and filtered through a neutral alumina and activated charcoal plug. The filtrate was then concentrated down to afford 1.5g, 99.5 % as a brown solid. The compound (3j’) was analyzed by NMR and was moved onto the deprotection step.
- phosphorus trichloride (0.19 g, 1.40 mmol) and triethylamine (0.57 g, 5.62 mmol) were added to 50 mL of toluene in a 1 10 mL glass jar.
- the solution was placed in the glove box freezer (-35 °C) for 1 hour to chill.
- the indole 3j (0.86 g, 2.81 mmol g) was weighed into a 20 mL vial and dissolved in 10 mL of THF. The indole solution was also chilled in the glove box freezer for 1 hour.
- Triethylamine (0.12 g, 1.16 mmol) in toluene (5 mL) was added to the solution dropwise with stirring. The reaction mixture was allowed to stir at room temperature overnight. An aliquot of the reaction mixture was removed, filtered, and analyzed by 31 p NMR spectroscopy. The spectrum showed partial conversion to the desired product (5 104 ppm). Another 0.04 g of diol was added, the reaction stirred for another 24 h at room temperature. Once all the starting chloride was gone, the reaction mixture was filtered through Celite to remove triethylammonium chloride and the colorless filtrate was pumped down to dryness to yield a light brown solid. Alumina column was required to remove all the attendant by-products.
- phosphorus trichloride (0.26 ml_, 3.0 mmol) and triethylamine (2 mL, 14 mmol) were added to 60 mL of toluene in a 1 10-mL glass jar.
- the solution was placed in the glove box freezer (-35 °C) for 1 hour to chill.
- the 3-(3,5-dimethylphenyl)-1 /-/-indole 3k (1 .34 g, 6.04 mmol) was weighed into a 20-mL vial and dissolved in 10 mL of toluene.
- the indole solution was also chilled in the glove box freezer for 1 hour.
- the two solutions were removed from the freezer and the cold indole solution was added drop wise with stirring to the cold PCI 3 /NEt 3 solution. A copious amount of white precipitate formed during the addition.
- the reaction mixture was allowed to warm to room temperature and stir overnight. The next day, an aliquot of the reaction mixture was removed, filtered and analyzed by 31 p NMR spectroscopy. The reaction mixture was filtered through Celite to remove triethylammonium chloride and the pale-yellow filtrate was pumped down to dryness. The resultant white residue was triturated with 40 mL of hexanes to leave a white solid. The solid was dried under vacuum for 1 hour.
- the reaction mixture was allowed to stir at room temperature overnight. The next morning, an aliquot of the reaction mixture was removed, filtered, and analyzed by 31 P NMR spectroscopy. The spectrum showed good conversion to the desired product CL3 (105 ppm) in approximately 82% purity.
- the reaction mixture was filtered through Celite to remove triethylammonium chloride and the yellow filtrate was pumped down to dryness. The filtrate was loaded directly over to 330g silica column using liquid injection. Silica gel column was required to remove all of the attendant by-products. A 330 g gold silica gel column (5 - 25 % dichloromethane in hexane) was utilized to purify the product (CL3) with the rest of the side products; Overall yield: 47.3%.
- Examples 1 -13 and Comparative Examples 1 -3 [0082] In the following Examples 1 -13 and Comparative Examples 1 -3, reaction conversion, selectivity, and regioselectivity (N/l ratio) were measured by 1 H NMR in CgDg, product structures and composition were additionally supported by 1 3c NMR in CgDg.
- reaction mixtures were analyzed by 1 H and 13c NMR.
- Neat substrate hydroformylation involved either catalyst activation during the initial reaction period or catalyst pre-activation in toluene prior to hydroformylation, followed by the transfer of the activated catalyst to the particular substrate utilized.
- hydroformylation generated branched aldehydes i.e., isobutanal
- byproducts which were detected and analyzed by NMR.
- Reaction rates are expressed as moles of aldehyde produced per volume of catalyst solution per unit time (moles/L-hour) ; this value is additionally divided by the propylene partial pressure to help dampen the effects of small, unavoidable fluctuations in the propylene feed rate (rate/Olefin).
- Product selectivity is expressed as the ratio of linear (normal) aldehyde versus branched (iso) aldehyde (N: I).
- Examples 1 -13 and Comparative Examples 1 -3 follow a General Hydroformylation Procedure.
- a reactor is charged with Solvent 2 (20 mL) and sparged with N2 overnight.
- Stock solutions of rhodium final concentration 50 ppm Rh introduced as Rh(acac)(CO)2 and a specific Ligand (type and equivalents as defined in Table 6 below) are then added, and the resulting solution is sparged with 1 : 1 syn gas for 3-4 hours to generate an active Rh(Ligand)dicarbonyl hydride catalyst species and to remove the toluene overhead.
- Catalyst Stability The general hydroformylation procedure is run continuously for about one week for each of Examples 1-13 and Comparative Examples 1-3 to determine catalyst stability. The rate/Olefin is plotted versus time; the slope of the resulting line provides a quantitative measure of deactivation. A slope of zero indicates no catalyst deactivation; the greater the negative slope, the faster the rate of deactivation, which is undesirable.
- the present hydroformylation process provides one or more benefits over previously proposed processes; i.e., faster reaction rate, improved selectivity, improved stability, and lower catalyst loadings to achieve these.
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| US2462635A (en) | 1946-10-22 | 1949-02-22 | Gen Electric | Cyclic polymeric organoaminosilanes |
| US2676182A (en) | 1950-09-13 | 1954-04-20 | Dow Corning | Copolymeric siloxanes and methods of preparing them |
| US3243404A (en) | 1962-04-02 | 1966-03-29 | Gen Electric | Silyl amine processing aids for polysiloxane elastomers |
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| WO2023200935A1 (en) | 2023-10-19 |
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| KR20250004253A (en) | 2025-01-07 |
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| CN118019747A (en) | 2024-05-10 |
| US20250257088A1 (en) | 2025-08-14 |
| ZA202407838B (en) | 2026-01-28 |
| KR20250004254A (en) | 2025-01-07 |
| CN118946574A (en) | 2024-11-12 |
| JP2025512267A (en) | 2025-04-17 |
| WO2023200934A1 (en) | 2023-10-19 |
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